Porous synthetic resin molded part and method of producing the same

ABSTRACT

A method of producing a porous molded part includes a mixing process for mixing a granular porous organizer composed of a water-soluble compound, a porous forming assistant agent composed of a polyhydric alcohol, and a cross-linking agent composed of an organic peroxide with a thermoplastic resin composition having a glass transition temperature below 0° C. to obtain a molding material; a cross-linking and forming process for placing the molding material in a molding die and performing a heat press molding thereby progressing coincidentally a cross-linking reaction and a shape forming of a seal face to obtain a molded material; an extracting process for extracting the granular porous organizer from the molded material obtained in the cross-linking and forming process to obtain a porous molded part; and a drying process for drying the porous molded part obtained in the extracting process.

CROSS-REFERENCE TO RELATED APPLICATIONS

This is a continuation-in-part application of a prior application Ser.No. 12/877,323, filed Sep. 8, 2010, now abandoned.

BACKGROUND OF THE INVENTION AND RELATED ART STATEMENT

The present invention relates to a porous synthetic resin molded partand a method of producing the porous synthetic resin molded partpreferably used for a seal face of a self-inking stamp and the like.

Patent Reference has disclosed a conventional porous synthetic resinmolded part. The porous synthetic resin molded part is formed of athermoplastic resin or a thermosetting resin, and is used as a materialof a face of a self-inking stamp. The porous synthetic resin molded partis formed of a porous body with a porosity of 40% to 95% and Durometerhardness of 50 or higher.

Patent Reference: Japanese Patent Publication No. 2001-150780

Patent Reference has disclosed that a thermoplastic resin as a basematerial may contain a cross-linking agent such as an organic peroxide,so that the thermoplastic resin can be cross-linked through irradiatingultraviolet rays or radioactive rays. After the thermoplastic resin isformed in a sheet material, the sheet material is engraved with a laserto form a seal face. Accordingly, it is necessary to perform anengraving process to form the seal face after producing the sheetmaterial.

An object of the present invention is to provide a method of producing aporous synthetic resin molded part preferably used for a seal face of aself-inking stamp and the like without an engraving process.

SUMMARY OF THE INVENTION

In order to attain the object described above, according to the presentinvention, a method of producing a porous synthetic resin molded partincludes the steps of mixing a granular porous organizer composed of awater-soluble compound, a porous forming assistant agent composed of apolyhydric alcohol, and a cross-linking agent composed of an organicperoxide into a thermoplastic resin composition as a base material toobtain a molding material; injecting the molding material into a moldingdie; and performing a direct pressure molding (referred to as acompressive molding, a compression molding, or a heat press molding) at140° C. to 170° C. for 4 to 10 minutes for performing a cross-linkingreaction and forming a seal face coincidentally to obtain a molded part.

According the present invention, the method of producing a poroussynthetic resin molded part may further include an extracting step ofimmersing the molded part obtained in the step of performing the directpressure molding into heated water at 70° C. to 100° C. for extractingthe granular porous organizer to obtain the porous synthetic resinmolded part.

In the present invention, the direct pressure molding allows thecross-linking reaction and the shape forming of a seal face to progresscoincidentally. Therefore, a further engraving process becomes to beunnecessary, and it is enabled to provide a production method for poroussynthetic resin molded part preferable to be used for a self-inkingstamp face or the like.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a process chart showing a method of producing a poroussynthetic resin molded part according to an embodiment of the presentinvention.

DETAILED DESCRIPTION OF PREFERRED EMBODIMENTS

Embodiments of the present invention will be hereinafter described withreference to the drawing.

According to the present embodiment, as shown in FIG. 1, a method ofproducing a porous synthetic resin molded part includes: a mixingprocess ST1 for obtaining a molding material through mixing a granularporous organizer composed of a water-soluble compound, a porous formingassistant agent composed of a polyhydric alcohol, and a cross-linkingagent composed of an organic peroxide into a thermoplastic resincomposition as a base material; a cross-linking and forming process ST2for obtaining a molded material through placing or injecting the moldingmaterial into a molding die and performing a direct pressure molding(compressive molding, compression molding, or heat press molding) at140° C. to 170° C. for 4 to 10 minutes thereby progressingcoincidentally a cross-linking reaction and a shape forming of a sealface; an extracting process ST3 for obtaining a porous molded partthrough extracting the granular porous organizer from the moldedmaterial obtained in the cross-linking and forming process; and a dryingprocess ST4 for drying the porous molded part obtained in the extractingprocess.

In the present embodiment, the thermoplastic resin is a base material ofa self-inking stamp face, and preferably has a process temperature of110° C. or less. Examples of the thermoplastic resin include anethylene-vinyl acetate copolymer (EVA), a thermoplastic elastomer (TPE),low-density polyethylene (LDPE), linear low-density polyethylene(LLDPE), and the like. Among them, a preferred material is a metalloceneplastomer, synthesized with a metallocene catalyst, i.e., an ethylenealpha-olefin copolymer which has a low melting point, high flexibility,and good physical properties.

In the present embodiment, the granular porous organizer performs ashydraulic cores for forming interconnecting cells of the self-inkingstamp face, and is preferably a water-soluble compound in considerationof a solvent to be used in the extracting process ST3 for obtaining theporous molded part. Examples of the water-soluble compound includepolyhydric alcohols such as pentaerythritol and polyethylene glycol;sugars such as glucose, fructose and maltose; and water-soluble saltssuch as potassium chloride, sodium chloride, sodium sulfate andpotassium nitrate. The water-soluble compound may be used alone or acombination thereof.

Pentaerythritol used as the granular porous organizer contains 95% ormore of monopentaerythritol and 47% or more of hydroxyl group, and has amelting point (a temperature of starting to melt) of 180° C. or more. Agranularity of the granular porous organizer may be appropriatelyselected according to quality required for the self-inking stamp faceand a purpose. It is preferred that a grain diameter of the granularporous organizer as a 10% diameter thereof is approximately in a rangeof 10 μm to 12 μm, so that the self-inking stamp face has a fine anduniform porosity.

In the present embodiment, the cross-linking agent is capable ofcross-linking at least the thermoplastic resin to be used. Thecross-linking agent capable of cross-linking a synthetic resin includesdialkylperoxides, peroxy ketals, hydroperoxides, peroxy esters, and thelike. The cross-linking agent preferably has a high decompositiontemperature, so that the cross-linking agent can be heated approximatelyto 100° C. in a process of kneading the molding material.

When the cross-linking agent has an excessively high resolutiontemperature, it takes a longer time for the cross-linking. On the otherhand, when the cross-linking agent has an excessively low resolutiontemperature, the cross-linking agent starts to decompose during theprocess of kneading, thereby making it difficult to obtain a good moldedmaterial. Therefore, it is preferred that the maximum kneadingtemperature is 100° C. or more and the cross-linking agent has astandard cross-linking temperature approximately of 150° C. (140° C. to170° C.). Accordingly, the cross-linking agent is preferably selectedfrom peroxy ketals. It is noted that the cross-linking agent maygenerate odor from a decomposed substance thereof.

In the present embodiment, the assistant agent for extracting the porousorganizer includes a polyhydric alcohol. More specifically, theassistant agent includes a combination of a dihydric alcohol and atrihydric alcohol.

The dihydric alcohol includes polyethylene glycols, preferably apolyethylene glycol having an average molecular weight of 1,000 orhigher. Polyethylene glycol has an advantageous effect of functioning asan extracting assistant agent, and further functions as a dispersingagent in the process of kneading and dispersing pentaerythritol as theporous organizer into the thermoplastic synthetic resin.

The trihydric alcohol includes glycerin. Glycerin has an advantageouseffect as the extracting assistant agent, and further effectivelyimproves a tearing strength of the extracted material (the porous moldedpart). When only polyethylene glycol is used for extraction, theextracted material tends to have a low tearing strength or poordimensional stability due to swelling. Therefore, glycerin is preferablyused. When the combination of the dihydric alcohol and the trihydricalcohol is used in a good balance, it is possible to obtain the moldedpart with remarkable extractability, physicality and ink absorbability.

In the present embodiment, in addition to the thermoplastic resin, thecross-linking agent, the porous organizer, and the porous formingassistant agent, the molding material may contain a plasticizing agent,a surface activating agent, a pigment, a thermal stabilizer, alubricant, an ultraviolet absorbing agent, an antistatic agent, a fireretarding material, or an antiaging agent. It is preferred that such anadditive is added with 50 parts by weight or less with respect to 100parts by weight of the thermoplastic synthetic resin.

A mixing ratio of components in the mixing and dispersing process ST1 isas follows. Firstly, a ratio of the porous organizer and the porousforming assistant agent to 100 parts by weight of the thermoplasticsynthetic resin is in a range from 150 to 500 parts by weight. Whenmixing amounts of the porous organizer and the porous forming assistantagent increase, the number of pores in the porous molded part increases,thereby making it possible to obtain a soft molded part. On thecontrary, when the mixing amounts of the porous organizer and the porousforming assistant agent decrease, the number of the pores in the porousmolded part decreases, thereby making it possible to obtain a hardmolded part. The mixing amounts of the porous organizer and the porousforming assistant agent may be adjusted depending on an intended purposethereof, so that the number of the pores and the hardness can be set inaccordance with the intended purpose.

A ratio of the cross-linking agent is preferably in a range from one tofive parts by weight, more preferably in a range from one to two partsby weight, relative to 100 parts by weight of the thermoplasticsynthetic resin.

In the mixing and dispersing process ST1 according to the presentembodiment, the molding material is obtained through blending and mixinguniformly the thermoplastic resin composition, the granular porousorganizer, the porous forming assistant agent, and the cross-linkingagent, in addition to the additives if necessary. In the mixing anddispersing process ST1, an open roll mill, a heat/pressure kneader, anintensive mixer, a single spindle extruder, a double spindle extruder,an internal mixer, a co-kneader, or a continuous kneading machine withdouble spindle rotor may be arbitrarily used.

In the cross-linking and forming process ST2 according to the presentembodiment, the molding material obtained in the mixing and dispersingprocess ST1 is filled in a molding die having a cavity corresponding toa shape of the self-inking stamp face. Then, a direct pressure molding(referred to as a compression molding or a heat press molding) isperformed under a specific condition (described later), so that across-linking reaction and a shape forming of the seal face areperformed coincidentally.

A temperature for the cross-linking reaction and the shape forming is ina range from 140° C. to 170° C. where the thermoplastic synthetic resincomposition melts thereby to soften, the porous forming assistant agentmelts or softens, and the cross-linking agent decomposes to produce across-linked substance. A time duration for the cross-linking andforming is in a range from four to 10 minutes with the inclusion ofpreheating, air evacuating and gas evacuating. If the temperature forthe cross-linking and forming exceeds 180° C., the cross-linkingreaction progresses fast. In this case, the cross-linking reactionexcessively progresses in the preheating stage, thereby making itdifficult to obtain a high-quality molded material. On the contrary, ifthe temperature for the cross-linking and forming is lower than 140° C.,the cross-linking reaction may not sufficiently complete. In this case,it may be difficult to remove a portion of the molded material from themolding die, thereby making it difficult to obtain a high-quality moldedmaterial. If the time duration for the cross-linking and forming isshorter than four minutes, the cross-linking reaction may not complete,thereby making it difficult to obtain a high-quality molded material. Onthe other hand, if the time duration for the cross-linking and formingexceeds ten minutes, the productivity becomes lower, thereby increasinga cost of the product.

In the cross-linking and forming process, the molding die includes ametal molding die made of aluminum, iron or the like, or a syntheticresin molding die made of phenol resin, ebonite or the like. Forexample, a commercially available resin material (e.g. Fuji Torelief, aproduct of FUJIFILM Corporation, Rigilon, a product of Tokyo Ohka KogyoCo., Ltd.) may be used for the synthetic resin molding die. When themetal molding die is made of copper or an alloy thereof such as brass,copper tends to inhibit the cross-linking reaction, so that the metalmolding die may not be suitable. According to the present embodiment,the molding die is formed with a pattern in accordance with characters,figures or designs of the stamp face, thereby forming the stamp face.Accordingly, it is unnecessary to perform an additional engravingprocess.

In the cross-linking and forming process, a direct pressure moldingmachine includes a heat press machine to be usually used forcross-linking a rubber, and a pressing capability thereof may beapproximately within a range from 10 to 50 tons. While it is enough toheat up to approximately 200° C., an accurate temperature control isrequired.

In the cross-linking and forming process, after pre-heating the moldingdie to be used to a molding temperature, the molding material in apellet-form is uniformly filled in the molding die. Then, the moldingmaterial is molded to obtain the molded material under the pressing andheating condition for four to 10 minutes through pre-heating, pressing,air evacuating and gas evacuating in this order. The molded material isremoved from the molding die after being cooled down to a range from 30°C. to 50° C. of a surface temperature thereof. The molding materialcontains the porous organizer and the porous forming assistant agent notcross-linked. Particularly, the porous forming assistant agent has amelting point within the range from 50° C. to 60° C. Therefore, it isenabled to stabilize a shape of the molded material by releasing thesame from the molding die after cooling down below the melting point.

In the extracting process of the porous organizer ST3, the porousforming assistant agent, and a residue thereof are removed from themolded material obtained through the cross-linking and forming processusing an extracting solvent. The extracting solvent to be used in thepresent process preferably includes water due to an easy post processand a lower cost. When the molded material is immersed into water as theextracting solvent, it is possible to extract the porous organizer andthe porous forming assistant agent from the molded material.

According to the present embodiment, the molded material is cross-linkedto have a good thermal stability. Therefore, even though extracting withwater having a temperature in a range from a room temperature to 100°C., preferably from 70° C. to 100° C., the porosity of the moldedmaterial may not be damaged. The temperature of water is appropriatelyselected depending on a type of thermoplastic resin composing the basematerial. When the molded material is cross-linked, as opposed to amolded material having a same composition without being cross-linked, itis possible to extract in a several fold fast time duration due to theheating effect. Therefore, it is possible to shorten the time requiredfor the extracting process, thereby making it possible to quicklydeliver a product. When the molded material with a general compositionfor the self-inking stamp face has a thickness of approximately 3 mm, itis possible to extract 93% or more under a condition of 70° C.×3 hours,while the time depends on the thermoplastic resin composition, and thesize and the thickness of the molded material.

In the drying process ST4, the extract (the molded material) may bedried through natural drying for a long time to complete. The dryingtime may be shortened to several hours using a warm air drier or adehumidification drier. A drying temperature may be in a range from 20°C. to 100° C., preferably in a range from 50° C. to 60° C. for one totwo hours. When the molded material has the thickness of approximately 3mm, the drying process may be completed at 60° C. for two hours.

As described above, according to the production method of the presentembodiment, the direct pressure molding of the molding materialincluding the cross-linking agent allows the cross-linking reaction andthe shape forming of the seal face to progress coincidentally.Therefore, a further engraving process is unnecessary. Moreover, themolded material is immersed into hot water nearly equal to boiling waterin the extracting process of the porous organizer and the porous formingassistant agent. Therefore, it is enabled to shorten the extractingtime.

Furthermore, the porous synthetic resin molded part obtained through theprocesses has the porosity depending on the amount of the porousorganizer contained in the molding material, and becomes the body withuniform interconnecting cells. In addition, the thermoplastic resincomponent as the base material is cross-linked, so that physicalcharacteristics such as heat resistance, abrasion resistance and tensionstrength are strengthened compared with those of the thermoplastic resincomposition as a raw material. Accordingly, it is expected to use theporous synthetic resin molded part in an application requiring heatresistance and abrasion resistance.

An experiment for evaluating the porous synthetic resin molded part willbe explained next.

First Embodiment

In the evaluation, a first example was prepared as follows. 200 parts byweight of fine powder pentaerythritol as the granular porous organizer,25 parts by weight of powder type polyethylene glycol as the firstassistant agent, 10 parts by weight of glycerin as the second assistantagent, 0.1 part by weight of red organic pigment, and 5 parts by weightof the cross-linking agent were added into 100 parts by weight of linearlow-density polyethylene (LLDPE) having a glass transition temperaturebetween −110° C. and −20° C., and were mixed for five minutes using ahigh speed super mixer, thereby obtaining a uniform mixture. The mixturewas kneaded using a double spindle extruder, thereby obtaining a moldingmaterial.

Second Embodiment

In the evaluation, a second example was prepared as follows. 200 partsby weight of fine powder pentaerythritol, 25 parts by weight of powdertype polyethylene glycol, 10 parts by weight of glycerin, 0.1 part byweight of red organic pigment, and 5 parts by weight of peroxy ketal asthe cross-linking agent were added into 100 parts by weight oflow-density polyethylene (LDPE) having a glass transition temperaturebetween −120° C. and −20° C., and were mixed for five minutes using ahigh speed super mixer, thereby obtaining a uniform mixture. The mixturewas kneaded using a double spindle extruder, thereby obtaining a moldingmaterial.

Third Embodiment

In the evaluation, a third example was prepared as follows. 200 parts byweight of fine powder pentaerythritol, 25 parts by weight of powder typepolyethylene glycol, 10 parts by weight of glycerin, 0.1 part by weightof red organic pigment, and 5 parts by weight of peroxy ketal as thecross-linking agent were added into 100 parts by weight of an ethylenealpha-olefin copolymer metallocene plastomer having a glass transitiontemperature between −120° C. and 0° C., and were mixed for five minutesusing a high speed super mixer, thereby obtaining a uniform mixture. Themixture was kneaded using a double spindle extruder, thereby obtaining amolding material.

First Comparative Example

In the evaluation, a first comparative example was prepared as follows.200 parts by weight of fine powder pentaerythritol as the granularporous organizer, 25 parts by weight of powder type polyethylene glycolas the first assistant agent, 10 parts by weight of glycerin as thesecond assistant agent, and 0.1 part by weight of red organic pigmentwere added into 100 parts by weight of linear low-density polyethylene(LLDPE) having a glass transition temperature between −110° C. and −20°C., and were mixed for five minutes using a high speed super mixer,thereby obtaining a uniform mixture. It should be noted that the firstcomparative example did not contain the cross-linking agent. Othercompositions of the first comparative example were the same as those inthe first example. The mixture was kneaded using a double spindleextruder, thereby obtaining a molding material.

Second Comparative Example

In the evaluation, a second comparative example was prepared as follows.200 parts by weight of fine powder pentaerythritol, 25 parts by weightof powder type polyethylene glycol, and 10 parts by weight of glycerin,0.1 part by weight of red organic pigment were added into 100 parts byweight of low-density polyethylene (LDPE) having a glass transitiontemperature between −120° C. and −20° C., and were mixed for fiveminutes using a high speed super mixer, thereby obtaining a uniformmixture. It should be noted that the second comparative example did notcontain the cross-linking agent. The mixture was kneaded using a doublespindle extruder, thereby obtaining a molding material.

Third Comparative Example

In the evaluation, a third comparative example was prepared as follows.200 parts by weight of fine powder pentaerythritol, 25 parts by weightof powder type polyethylene glycol, 10 parts by weight of glycerin, and0.1 part by weight of red organic pigment were added into 100 parts byweight of an ethylene alpha-olefin copolymer metallocene plastomerhaving a glass transition temperature between −120° C. and 0° C., andwere mixed for five minutes using a high speed super mixer, therebyobtaining a uniform mixture. It should be noted that the thirdcomparative example did not contain the cross-linking agent. The mixturewas kneaded using a double spindle extruder, thereby obtaining a moldingmaterial.

Fourth Comparative Example

In the evaluation, a first comparative example was prepared as follows.45 parts by weight of cone powder as the granular porous organizer wasadded into 190 parts by weight of an acetal polyvinylformal-melamineresin having a glass transition temperature between 55° C. and 100° C.,and were mixed for five minutes using a high speed super mixer, therebyobtaining a uniform mixture. It should be noted that the fourthcomparative example did not contain the assistant agent and thecross-linking agent. The mixture was kneaded using a double spindleextruder, thereby obtaining a molding material.

Fifth Comparative Example

In the evaluation, a first comparative example was prepared as follows.350 parts by weight of anhydrous sodium sulfate as the granular porousorganizer was added into 100 parts by weight of poly methyl methacrylate(PMMA) having a glass transition temperature between 70° C. and 105° C.,and were mixed for five minutes using a high speed super mixer, therebyobtaining a uniform mixture. It should be noted that the fifthcomparative example did not contain the assistant agent and thecross-linking agent. The mixture was kneaded using a double spindleextruder, thereby obtaining a molding material.

Sixth Comparative Example

In the evaluation, a third comparative example was prepared as follows.500 parts by weight of sodium chloride as the granular porous organizer,40 part by weight of a styrene solution, and 1.0 part by weight ofperoxyl benzoyl were added into 60 parts by weight of an unsaturatedpolyester resin having a glass transition temperature between 70° C. and130° C., and were mixed for five minutes using a high speed super mixer,thereby obtaining a uniform mixture. It should be noted that the sixthcomparative example did not contain the assistant agent. The mixture waskneaded using a double spindle extruder, thereby obtaining a moldingmaterial.

Molding

The molding material was cross-linked and formed (molded) using a directpressure molding machine. The molding temperature was in the range from140° C. to 170° C., and the time duration was five minutes. It is to benoted that the molding temperature and the molding time was set as anoptimum condition in accordance with sizes of a character, a symbol anda design of a resin molding die. In general, a preferred temperature wasin a lower region of the range from 145° C. to 155° C., in a case of asize mark character stamp with a larger character, symbol or design. Thepreferred temperature was in a higher region of the range from 155° C.to 165° C. in a case of a ball mark character stamp with a smallercharacter, symbol or design. The molded material was immersed into hotwater at 70° C. for three minutes (the extracting process), and thendried for two hours using a warm air drier (the drying process).

Evaluation

In order to evaluate the heat resistance of the porous synthetic resinmolded part, the porous molded material was cut in chips of self-inkingstamp faces each with a thickness of 2.7 mm and an area of 30 mm square.The chips were immersed into boiling water for 5 minutes, 10 minutes, 20minutes, and 30 minutes, respectively, before drying the chips.

In order to confirm the interconnecting cells and evaluate heatresistance thereof, a commercially available oil-based black pigment ink(available from Taiyotomah Co., Ltd.) was absorbed from a bottom surfaceof the chip, and a time duration was measured until an upper surface ofthe chip became entirely black. The number of test specimen was three.Results thereof are shown in Table 1.

The chips made from the first to third comparative examples were shrunkand became small after one to three minutes of the treatment in boilingwater. In spite of trying to absorb the ink from the bottom surface ofthe chip, there was no ink infiltration toward the upper surface of thechip. From this result, it was considered that the interconnecting cellswere destroyed. In the samples without immersing into boiling water(zero minute), the time duration was from 13 to 100 minutes. Resultsthereof are shown in Table 1.

From the results shown in Table 1, it was confirmed that there was nosignificant difference in the ink absorption time between the samplestreated in boiling water (5, 10, 20, and 30 minutes) and the samples nottreated in boiling water (zero minute). Accordingly, the interconnectingcells were certainly formed, and not destroyed after the heat treatment.

TABLE 1 Heat resistance Treatment time 0 min 5 min 10 min 20 min 30 minExample 1 13-18 min 15-18 min 10-17 min 10-16 min 10-13 min Example 2 16min 25 min 35 min 35 min 35 min Example 3 100 min 110 min 110 min 110min 110 min Comparative 13-18 min shrunk (3 min) example 1 Comparative16 min shrunk (1 min) example 2 Comparative 100 min shrunk (3 min)example 3

In order to evaluate sequential stampability, a ball mark stamp face wasprepared using a resin molding die under the condition described above.After an oil-based black ink was sufficiently absorbed into the porousmolded part thus obtained, the porous molded part sequentially stampedonto white papers without refilling the ink, and the number of thestamps was measured. Similarly, a size mark stamp face was preparedusing a resin molding die under the condition described above. After analcohol-based blue dye ink was sufficiently absorbed in the porousmolded part, the porous molded part sequentially stamped ontopolyethylene bags without refilling the ink, and the number of thestamps was measured.

In the examples No. 1 to No. 3 and the comparative examples No. 1 to No.3, when the ball mark stamp face stamped 1,000 times onto copy papers ofA4 size, stamped ink seemed to be slightly diluted but decipherable.When the size mark stamp face stamped 700 times onto polyethylene (PP)bags, stamped ink seemed to be slightly diluted but decipherable.However, in the comparative examples No. 4 to No. 6, the ball mark stampface could stamped only five times onto copy papers of A4 size andpolyethylene (PP) bags. Results thereof are shown in Table 2.

In order to evaluate organic solvent resistance of the porous syntheticresin molded part, the porous molded material was cut in chips ofself-inking stamp faces each with a thickness of 2.7 mm and an area of30 mm square to prepare samples. The chips were immersed into ethylalcohol, isopropyl alcohol (IPA), n-hexane, and toluene at a roomtemperature for five hours, and then were removed from the solvents.

In order to confirm the interconnecting cells of the chips after beingimmersed into the organic solvents, an oil-based black ink was absorbedfrom a bottom surface of the chip, and a time duration was measureduntil an upper surface of the chip became entirely black. Forcomparison, the time duration was measured with respect to the chip notimmersed into the organic solvent (without treatment).

As a result, it took nine minutes to absorb the ink in the chip notimmersed into the organic solvent. Further, it took seven minutes toabsorb the ink in the chip immersed in ethyl alcohol, six minutes toabsorb the ink in the chip immersed in isopropyl alcohol, seven minutesto absorb the ink in the chip immersed in n-hexane, and 11 minutes toabsorb the ink in the chip immersed in toluene. In addition, the chipsimmersed into n-hexane and toluene were swollen and enlarged, andreturned to original sizes after removed from the organic solvents. Thechips immersed into ethyl alcohol and isopropyl alcohol (IPA) exhibitedno change in size. From the results, it was confirmed that theinterconnecting cells were not destructed in the organic solvents.Results thereof are shown in Table 2.

In order to determine Durometer hardness of the porous synthetic resinmolded part, the porous molded material was subject to the type-CDurometer and the type-O Durometer according to ASTM D-2240. Resultsthereof are shown in Table 2. As shown in Table 2, it is confirmed thatthe first to third examples exhibit the proper Durometer hardness.

TABLE 2 Organic solvent Durometer Sequential resistance (min) hardnessstampability ethyl n- tolu- type- type- A4 PP alcohol IPA hexane ene C OExample 1000 700 7 6 7 11 30 75 No. 1 Example 1000 700 28 52 27 20 30 75No. 2 Example 1000 700 180 87 180 11 10 45 No. 3 Compar. 1000 700 7 6 711 20 65 Example No. 1 Compar. 1000 700 28 52 27 20 20 65 Example No. 2Compar. 1000 700 180 87 180 11 10 40 Example No. 3 Compar. 5 5 72 90Example No. 4 Compar. 5 5 80 90 Example No. 5 Compar. 5 5 86 90 ExampleNo. 6

As shown in Table 2, in the examples No. 1 to No. 3, when the materialhaving a low glass transition temperature (between −120° C. and 0° C.)is used as the thermoplastic resin composition, it is possible to obtainthe excellent sequential stampability due to the low Durometer hardness.On the other hand, in the comparative examples No. 4 to No. 6, when thematerial having a high glass transition temperature such as PMMA and theunsaturated polyester resin, it is difficult to obtain the goodSequential stampability due to the high Durometer hardness.

As shown in Table 1 and Table 2, only the examples No. 1 to No. 3exhibit the balanced properties such as the heat resistance, thesequential stampability, and the solvent resistance.

What is claimed is:
 1. A porous synthetic resin molded part, comprising:a granular porous organizer composed of pentaerythritol, a first porousforming assistant agent composed of polyethylene glycol, a second porousforming assistant agent composed of glycerin, a cross-linking agentcomposed of an organic peroxide; and a thermoplastic resin having aglass transition temperature below 0° C., wherein said granular porousorganizer is contained at an amount double of that of the thermoplasticresin, and said second porous forming assistant agent is contained at anamount one tenth of that of the thermoplastic resin.
 2. The poroussynthetic resin molded part according to claim 1, wherein saidthermoplastic resin is composed of at least one of an ethylene-vinylacetate copolymer, a thermoplastic elastomer, low-density polyethylene(LDPE), linear low-density polyethylene (LLDPE), and an ethylenealpha-olefin copolymer.
 3. The porous synthetic resin molded partaccording to claim 1, wherein said thermoplastic resin is adjusted sothat the porous synthetic resin molded part has Durometer hardness oftype-O below 75 according to ASTM D-2240.
 4. The porous synthetic resinmolded part according to claim 1, wherein said cross-linking agent has across-linking temperature between 140° C. and 170° C.